Thermally bondable fiber for high strength non-woven fabrics

ABSTRACT

Thermobondable fiber of at least one first component of polypropylene having a melt flow rate of 0.5-30, and at least one second component of polypropylene having a melt flow rate of 60-1000.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a division of application Ser. No. 08/003,696, filed Jan. 13, 1993, U.S. Pat. No. 5,629,080, which is a continuation-in-part of application Ser. No. 07/943,190, filed Sep. 11, 1992, now abandoned, which is a continuation-in-part of application Ser. No. 07/818,772, filed Jan. 13, 1992, now abandoned.

This application is related to application Ser. No. 07/474,897, filed Feb. 5, 1990, now abandoned, in the name of Kozulla, its continuation application Ser. No. 07/887,416, filed May 20, 1992, now U.S. Pat. No. 5,281,378, its continuation-in-part application Ser. No. 07/683,635, filed Apr. 11, 1991, now U.S. Pat. No. 5,318,735, and its divisional application Ser. No. 07/836,438, filed Feb. 18, 1992, now abandoned, and its continuation application Ser. No. 07/939,857, now U.S. Pat. No. 5,431,994, filed Sept. 2, 1992, the disclosures of which are hereby incorporated by reference in their entirety.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to synthetic fibers used in the manufacture of non-woven fabrics. In particular, the present invention relates to polypropylene fibers intended for such use, processes of producing polypropylene fibers, compositions for producing polypropylene fibers, non-woven fabrics produced with polypropylene fibers, and articles containing polypropylene fibers.

2. Background Information

The production of polypropylene fibers and filaments usually involves the use of a mix of a single polymer with nominal amounts of stabilizers and pigments. The mix is melt extruded into fibers and fibrous products using conventional commercial processes. Non-woven fabrics are typically made by making a web of the fibers, and then thermally bonding the fibers together where they meet. More specifically, staple fibers are converted into non-woven fabrics using, for example, a carding machine, and the carded fabric is thermally bonded. The thermal bonding can be achieved using various heating techniques, including heating with heated rollers and heating through the use of ultrasonic welding.

Conventional thermally bonded non-woven fabrics exhibit good loft and softness properties, but less than optimal cross-directional strength, and less than optimal cross-directional strength in combination with high elongation. The strength of the thermally bonded non-woven fabrics depends upon the orientation of the fibers and the inherent strength of the bond points.

Over the years, improvements have been made in fibers which provide stronger bond strengths. However, further improvements are needed to provide even higher fabric strengths to permit use of these fabrics in today's high speed converting processes for hygiene products, such as diapers and other types of incontinence products. In particular, there is a need for a thermally bondable fiber and a resulting nonwoven fabric that possess high cross-directional strength and high elongation. Additionally, there is a need for a one-step process for making staple fiber known as a "short spin" process that provides filaments and fibers with properties as good as those produced by a two-step process called a "long spin" process.

SUMMARY OF THE INVENTION

Accordingly, it is an object of the present invention to provide a thermally bondable fiber and a resulting nonwoven fabric that possesses high cross directional strength and high elongation. Additionally, it is an object of the present invention to provide a "short spin" process that provides filaments and fibers that have properties that have qualities that are as good as those produced by a "long spin" process.

The object of the present invention is achieved by providing a fiber comprising at least one polypropylene having a melt flow rate of about 0.5-30, and at least one polypropylene having a melt flow rate of about 60-1000.

Preferably, based on the weight of the fiber, the fiber comprises at least about 3.0% by weight of the at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 3.0% by weight of the at least one polypropylene having a melt flow rate of about 60-1000. More preferably, based on the weight of the fiber, the fiber comprises at least about 10.0% by weight of the at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 10.0% by weight of the at least one polypropylene having a melt flow rate of about 60-1000. Preferably, the fiber comprises at least one polypropylene having a melt flow rate of about 1-25, and at least one polypropylene having a melt flow rate of about 200-1000.

Preferably, based on the weight of the fiber, the at least one polypropylene having a melt flow rate of about 0.5-30 is present in an amount of about 5-95%, and the at least one polypropylene having a melt flow rate of about 60-1000 is present in an amount of about 5-95%. More preferably, the fiber comprises about 2-5% by weight, preferably about 3% by weight, of polypropylene having a melt flow rate of about 0.5-5, preferably about 0.8-5.0, and more preferably about 1.0-3.0, about 70-85% by weight, preferably about 75% by weight, of polypropylene having a melt flow rate of about 10-20, preferably about 10-15, and about 10-28% by weight, preferably about 22% by weight, of polypropylene having a melt flow rate of about 300-600, preferably about 350-450.

The fiber according to the present invention has an average rheological polydispersity index of at least about 4.5, preferably at least about 5.0, more preferably about 5.5, and a preferred range of about 5.0-7.0. Further, the fiber has a viscoelastic constant of about 1.5-2.0, a fiber elongation of at least about 250%, a fiber tenacity less than about 2.5 g/denier, and a size less than about 5 dpf. As utilized in this application dpf denotes denier per filament, with denier being defined as weight in grams per 9,000 meter length of filament.

The fiber can contain at least one additive, and the at least one additive can comprise at least one stabilizer.

It is an additional object of the present invention to provide a composition comprising at least one polypropylene having a melt flow rate of about 0.5-30, preferably, about 1-25, and at least one polypropylene having a melt flow rate of about 60-1000, preferably, about 200-1000. This composition can contain similar components and have similar characteristics as the above-described fiber. For example, the composition can have an average rheological polydispersity index of at least about 4.5, preferably of at least about 5.0, more preferably at least about 5.5, and a preferred range of about 5.0-7.0, and can contain at least one additive, such as at least one stabilizer.

Also, the composition can comprise, based on the weight of the composition, at least one polypropylene having a melt flow rate of about 0.5-30 present in an amount of about 5-95%, and at least one polypropylene having a melt flow rate of about 60-1000 is present in an amount of about 5-95%. Preferably, based on the weight of the composition, the composition comprises at least about 3.0% by weight of the at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 3.0% by weight of the at least one polypropylene having a melt flow rate of about 60-1000. More preferably, based on the weight of the composition, the composition comprises at least about 10.0% by weight of the at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 10.0% by weight of the at least one polypropylene having a melt flow rate of about 60-1000.

Preferably, the composition comprises about 2-5% by weight, preferably about 3% by weight of polypropylene having a melt flow rate of about 0.5-5, preferably about 0.8-5, and more preferably about 1.0-3.0, about 70-85% by weight, preferably about 75% by weight, of polypropylene having a melt flow rate of about 10-20, preferably about 10-15, and about 10-28% by weight, preferably about 22% by weight, of polypropylene having a melt flow rate of about 300-600, preferably about 350-450.

It is also an object of the present invention to provide a polypropylene containing fiber comprising a mixture of at least two components, the at least two components comprising at least one first component of polypropylene having a melt flow rate of about 0.5-30, and at least one second component of polypropylene having a melt flow rate of about 60-1000, preferably about 200-1000, and the fiber having an average melt flow rate of about 5-40, preferably about 10-30, and more preferably about 15-25.

It is also an object of the present invention to provide a polypropylene containing fiber having an average melt flow rate of about 5-40, preferably 10-30 and more preferably about 15-25, and containing at least about 3.0% of at least one polypropylene having a melt flow rate of about 200-1000, and preferably containing at least about 10% of the at least one polypropylene having a melt flow rate of about 200-1000.

It is also an object of the present invention to provide a polypropylene containing fiber having an average rheological polydispersity index of at least about 4.5, preferably of at least about 5.0, more preferably of at least about 5.5, and a preferred ranged of about 5.0 to 7.0, and containing at least about 3.0% of at least one polypropylene having a melt flow rate of about 200-1000, and preferably containing at least about 10% of the at least one polypropylene having a melt flow rate of about 200-1000. Preferably, the polypropylene containing fiber has an average melt flow rate of about 5-40, more preferably about 10-30, and most preferably about 15-25.

It is yet another object of the present invention to provide a thermobondable polypropylene fiber, the fiber comprising components having a zero shear viscosity of at least about 2.0×10⁴ poise, and a viscoelastic constant of at least about 1.5.

The present invention is also directed to a thermally bondable fiber, the fiber having an average rheological polydispersity index of at least about 5.0, preferably of at least about 5.5, and a preferred range of about 5.0-7.0.

The thermobondable polypropylene fiber according to present invention as above-described in each of its different aspects has a substantially uniform morphology. This substantially uniform morphology is demonstratable by the above-described fibers being substantially uniformly stainable with ruthenium tetroxide.

Still further, it is an object of the present invention to provide a process for spinning polypropylene containing filaments comprising melt spinning a polypropylene composition having a broad molecular weight distribution through at least one spinnerette to form molten polypropylene containing filaments; and quenching the molten polypropylene containing filaments to obtain polypropylene containing filaments having an average Theological polydispersity index of at least about 5.0, preferably of at least about 5.5, and a preferred range of about 5.0-7.0. The spinning speed can be about 30 to 200 meters per minute, preferably about 80-100 meters per minute, and the polypropylene containing filaments can be continuously drawn and crimped, as practiced with a "short spin; process. Alternatively, the spinning speed can be about 500 to 2500 meters per minute, preferably about 1100-2000 meters per minute, and the polypropylene containing filaments can be drawn and crimped at a speed of about 50 to 250 meters per minute, preferably about 150-200 meters per minute, in a second step, as practiced with a "long spin" process.

The quenching according to the process according to the present invention can be effected to obtain a substantially immediate cooling of the molten polypropylene containing filaments as the molten polypropylene containing filaments exit the at least one spinnerette. Preferably, the quench comprises an air quench having a velocity, for a "short spin" process, of about 10-45 meters/second, preferably about 25-35 meters/second, and more preferably about 30 meters/second; and, for a "long spin" process, of about 1.5-4.0 meters/second, preferably about 2.0 meters/second. The quench air temperature is about 10°-40° C., preferably about 15°-30° C., and more preferably either about 15°-20° C. or about 37° C.

Still further, it is an object of the present invention to provide a process for spinning polypropylene containing filaments comprising melt spinning a polypropylene containing composition having a broad molecular weight distribution through at least one spinnerette at a spinning speed of about 30 to 200 meters per minute, preferably about 80-100 meters per minute, to form molten polypropylene containing filaments; and quenching the molten polypropylene containing filaments. Preferably, the quenched filaments have an average rheological polydispersity index of at least about 4.5, more preferably of at least about 5.0, even more preferably of at least about 5.5, and a preferred range of 5.0-7.0. Preferably, the polypropylene containing composition comprises at least one polypropylene having a melt flow rate of about 0.5-30, and at least one polypropylene having a melt flow rate of about 60-1000.

Still further, the present invention is directed to a process for producing thermobondable filaments having an average rheological polydispersity index of at least about 4.5, preferably at least about 5.0, and more preferably about 5.0-7.0 which is substantially maintained throughout the process, comprising melt spinning a polypropylene containing composition having a broad molecular weight distribution with an average Theological polydispersity index of at least about 4.5, preferably of at least about 5.0, more preferably of at least about 5.5, and a preferred range of about 5.0-7.0, through at least one spinnerette to form molten polypropylene filaments; and quenching the molten polypropylene filaments under conditions to obtain filaments having an average Theological polydispersity index substantially corresponding to the Theological polydispersity index of the polypropylene containing composition. This process can use the spinning speeds, drawing and crimping, and quenching steps as described throughout the disclosure.

Still further, the present invention is directed to a process for producing thermobondable filaments having an average rheological polydispersity index of at least about 4.5, preferably of at least about 5.0, more preferably of at least about 5.5, and a preferred range of about 5.0-7.0, which is substantially maintained throughout the process, comprising melt spinning a polypropylene containing composition having a broad molecular weight distribution through at least one spinnerette to form molten polypropylene containing filaments; and quenching the molten polypropylene containing filaments under conditions to maintain a substantially uniform morphology of the quenched polypropylene containing filaments having an average rheological polydispersity index substantially corresponding to the rheological polydispersity index of the polypropylene containing composition. This process can again use the spinning speeds, drawing and crimping, and quenching steps as previously described.

Still further, it is an object of the present invention to provide a process for spinning polypropylene containing filaments comprising melt spinning a polypropylene containing composition having a broad molecular weight distribution through at least one spinnerette at a spinning speed of about 30 to 200 meters per minute, preferably 80 to 100 meters per minute, to form molten polypropylene containing filaments; and quenching the molten polypropylene containing filaments to obtain polypropylene containing filaments having an average Theological polydispersity index of at least about 4.5, preferably of at least about 5.0, more preferably of at least about 5.5. Preferably, the filaments have an elongation greater than about 250%. Further, the polypropylene containing composition preferably contains at least about 3.0%, preferably at least about 10.0%, of at least one polypropylene having a melt flow rate of about 60-1000, preferably of about 200-1000. Preferably, the filaments have an average melt flow rate of about 5-40, more preferably an average melt flow rate of about 10-30, and most preferably an average melt flow rate of about 15-25.

Still further, it is an object of the present invention to provide a process for spinning polypropylene containing filaments comprising melt spinning a polypropylene containing composition having a broad molecular weight distribution, and containing at least about 3.0%, preferably at least about 10.0%, of at least one polypropylene having a melt flow rate of about 60-1000, preferably a melt flow rate of about 200-1000, through at least one spinnerette at a spinning speed of about 30 to 200 meters per minute, preferably of about 80-100 meters per minute, to form molten polypropylene containing filaments; and quenching the molten polypropylene containing filaments to obtain polypropylene containing filaments having an average melt flow rate of about 5-40. Preferably, the filaments have an average rheological polydispersity index is at least about 4.5, more preferably of at least about 5.0, even more preferably of at least about 5.5, and an elongation greater than about 250%.

It is also an object of the present invention to provide non-woven material comprising fibers as described above that are thermally bonded together; and to provide products having at least one layer of a non-woven material according to the present invention; and to provide hygienic products, including diapers, incontinence products and sanitary napkins, comprising at least one absorbent layer, and at least one non-woven fabric comprising nonwoven material of the invention and fibers as above-described thermally bonded together. Further, articles according to the present invention can include at least one liquid impermeable layer. For example, the diaper according to the present invention can include an outer impermeable layer, an inner nonwoven fabric layer comprising fibers according to the present invention, and an intermediate absorbent layer.

Still further, it is an object of the present invention to provide a nonwoven material comprising polypropylene containing fibers having an average melt flow rate of about 5-40, preferably about 10-30, more preferably about 15-25, and containing at least about 3.0%, preferably at least about 10.0%, of at least one polypropylene having a melt flow rate of about 60-1000, preferably a melt flow rate of about 200-1000, thermally bonded together.

Still further, it is an object of the present invention to provide a nonwoven material comprising polypropylene containing fibers having an average Theological polydispersity index of at least about 4.5, preferably about 5.0, more preferably about 5.5, and a preferred range of about 5.0-7.0, and containing at least about 3.0%, preferably at least about 10.0%, of at least one polypropylene having a melt flow rate of about 60-1000, preferably having a melt flow rate of about 200-1000, thermally bonded together. Preferably, the polypropylene containing fiber has an average melt flow rate of about 5-40, more preferably about 10-30, and most preferably about 15-25.

Because the fiber of the present invention provides superior bond strength compared with conventional polypropylene fiber, the nonwoven material thus produced exhibits superior cross-directional tensile properties. Further, nonwoven material produced with the fiber of the present invention has superior elongation, uniformity, loftiness, white coloration and softness, while exhibiting the above-noted superior mechanical properties.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

As used herein, polypropylene is utilized in its ordinary commercial meaning wherein the polypropylene is a substantially linear molecule. Further, as used herein, a polypropylene composition includes a material which contains a broad molecular weight distribution of linear polypropylene to enable the obtaining of fibers and filaments which have superior spinning and thermal bonding characteristics. Moreover, the fibers and filaments of the present invention provide non-woven materials of exceptional cross-directional strength, elongation, uniformity, loftiness and softness, by utilizing the disclosed polypropylene compositions including the disclosed linear polypropylene components having a broad molecular weight distribution, whether or not other components are present therein.

Further, as used herein, polypropylene includes homopolymers of propylene, various polymers containing propylene, such as copolymers and terpolymers of propylene, and polypropylene mixtures (including blends and alloys produced by mixing separate batches or forming a blend in situ) with other substances and polymers. For example, the polymer can comprise copolymers of propylene, and these copolymers can contain various components. Preferably, such copolymers include up to about 10 weight % of at least one of ethylene and butene, but can contain varying amounts thereof depending upon the desired fiber or filament.

By practicing the process of the present invention, utilizing spin compositions according to the present invention, fibers and filaments can be obtained which have superior spinning and thermal bonding characteristics. Moreover, the fibers and filaments of the present invention provide nonwoven materials of exceptional cross-directional strength, elongation, uniformity, loftiness and softness, by utilizing a material which contains a broad molecular weight distribution of linear polypropylene, whether or not other components are present therein.

The present invention is directed to various forms of fibers, including filaments and staple fibers. These terms are used in their ordinary commercial meanings. Typically, herein, filaments is used to refer to the continuous fiber on the spinning machine. "Staple fiber" is used to refer to cut fibers or filaments. Preferably, for instance, staple fibers for nonwoven fabrics useful in diapers have lengths of about 1 to 3 inches, more preferably 1.25 to 2 inches.

The polypropylene from which the improved fiber of the present invention can be produced includes at least one polypropylene having a melt flow rate of about 0.5-30, preferably about 1-25, and at least one polypropylene having a melt flow rate of about 60-1000, preferably about 200-1000. Preferably, based on the weight of the composition, the at least one polypropylene having a melt flow rate of about 0.5-30 is present in an amount of about 5-95%, and the at least one polypropylene having a melt flow rate of about 60-1000 is present in an amount of about 5-95%.

Preferably, based on the weight of the composition, the composition comprises at least about 3.0% by weight of the at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 3.0% by weight of the at least one polypropylene having a melt flow rate of about 60-1000. More preferably, based on the weight of the composition, the composition comprises at least about 10.0% by weight of the at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 10.0% by weight of the at least one polypropylene having a melt flow rate of about 60-1000.

More preferably, the composition comprises about 2-5% by weight, preferably, about 3% a melt ft of polypropylene having a melt flow rate of about 0.5-5, preferably about 0.8-5.0, and more preferably about 1.0-3.0, about 70-85% by weight, preferably about 75% by weight, of polypropylene having a melt flow rate of about 10-20, preferably about 10-15, and about 10-28% by weight, preferably about 22% by weight of polypropylene having a melt flow rate of about 300-600, preferably about 350-450.

In a particular embodiment of the invention, the polypropylene fiber can be made by blending at least one polypropylene having a melt flow rate of about 0.5-30, preferably about 1-25, and at least one polypropylene having a melt flow rate of about 60-1000, preferably about 200-1000 to form a composition, and then melt spinning the composition according to known procedures. The melt flow rate (MFR) as described herein is determined according to ASTM D-1238 (condition L;230/2.16).

The polypropylene to be made into fibers can comprise mixtures of more than one polypropylene within each defined MFR range. The melt flow rate of the mixture used to make the fiber of the present invention, as well as the fiber itself, has an average melt flow rate of about 5-40, preferably about 10-30, and more preferably about 15-25.

While the polypropylenes can be blended to obtain a broad mixture of molecular weights in the polypropylene to be produced into fibers, as an alternative to blending separate polymers to obtain the unique composition of the present invention, the components of the propylene to be produced into fibers can be made in situ by polymerizing propylene with or without ethylene or butane by known multi-reactor procedures, such as disclosed in Seiler and Goller, "Propylene (PP)," KUNSTSTOFFE 80 (1990) 10, pages 1085-1092, the disclosure of which is incorporated herein by reference.

Known processes for making staple fiber include a conventional "two-step long spin" process or "one-step short spin" process. The long spin process involves first melt-extruding fibers at typical spinning speeds of 500 to 1500 meters per minute. Typically, in a second step run at 100 to 250 meters per minute, these fibers are then drawn, crimped, and cut into staple fiber. The one-step short spin process involves conversion from polymer to staple fibers in a single step where typical spinning speeds are in the range of 50 to 200 meters per minute. The productivity of the one-step process is increased with the use of about 5 to 20 times the number of holes in the spinnerette compared to that typically used in the long spin process. For example, spinnerettes for a typical "long spin" process would include approximately 50-4,000, preferably approximately 3,000-3,500 holes, and spinnerettes for a typical "short spin" process would include approximately 4,000 to 100,000 holes preferably, about 30,000-70,000. Typical temperatures for extrusion of the spin melt are about 250°-300° C.

Other means of production of fibrous products include well known melt spun and melt blown processes, which provide continuous filaments-based non-woven fabrics and micro-denier staple-based non-woven fabrics, respectively. The fiber according to the present invention includes the long filamentous fibers made according to well known spun bond processes, as well as staple fibers made by the aforementioned short spin and long spin processes.

The fiber of the present invention has a preferable denier per filament (dpf) of no greater than about 5.0, preferably between about 0.5 and 3.0.

In making the fiber in accordance with the present invention, at least one stabilizer (including antioxidants) is preferably mixed with the polypropylene to be made into a fiber in an amount ranging from about 0.02-1.0 fiber-weight %, preferably about 0.05-0.2 fiber-weight %, in order to prevent deterioration of the fiber after production. Such stabilizers are well known in polypropylene-fiber manufacture and include phenylphosphites (available from General Electric Co. under the name ULTRANOX 626, and from Sandoz Chemical Co. under the name SANDOSTAB PEP-Q), N,N'-bis-piperidinyl diamine-containing materials (available from Ciba Geigy Corp. under the names CHIMASSORB 119 and CHIMASSORB 944), and hindered phenolics (available under the names CYANOX 1790 from American Cyanamid Co. and IRGANOX 1076 from Ciba Geigy Corp.) The at least one stabilizer can be mixed into the blend of polypropylenes, or can be separately added to polypropylenes that are to be mixed together to form a blend to be produced into fibers.

Optionally, whiteners, such as titanium dioxide, in amounts up to about 2 fiber-weight %, antiacids such as calcium stearate, in amounts ranging from about 0.05-0.2 fiber-weight %, colorants, in amounts ranging from 0.01-2.0%, and other well known additives are included in the fiber of the present invention. Wetting agents, such as disclosed in U.S. Pat. No. 4,578,414, incorporated herein by reference, are also usefully incorporated into the fiber of the present invention. Other commercially available useful additives include IRGAFOS 168 (available from American Cyanamid Co.), and LUPERSOL 101 (available from Pennwalt Corp.)

In making the fiber of the present invention, the polypropylene to be made into a fiber preferably includes about 5-95 fiber-weight % of polypropylene having a melt flow rate of about 0.5-30, and about 5-95 fiber weight % polypropylene having a melt flow rate of about 60-1000. Preferably, based on the weight of the composition, the at least one polypropylene having a melt flow rate of about 0.5-30 is present in an amount of about 5-95%, and the at least one polypropylene having a melt flow rate of about 60-1000 is present in an amount of about 5-95%. More preferably, the composition comprises about 2-5% by weight, preferably, about 3% by weight, of polypropylene having a melt flow rate of about 0.5-5, preferably about 0.8-5.0, more preferably about 1.0-3.0, about 70-85% by weight, preferably 75% by weight, of polypropylene having a melt flow rate of about 10-20, preferably about 10-15, and about 10-28% by weight, preferably about 22% by weight of polypropylene having a melt flow rate of about 300-600, preferably about 400.

Preferably, the fiber made in accordance with the present invention has an average rheological polydispersity index (PI) of at least about 4.5, preferably at least about 5.0, and more preferably between about 5.0 and 7.0 as measured according to Zeichner and Patel, Proceedings of Second World Congress of Chemical Engineering. Montreal. Vol. 6, pp. 333-337 (1981), incorporated herein by reference. In accordance with this reference, the dynamic shear property of a small polymeric sample subjected to a small amplitude oscillatory motion. The sample is held between two parallel plates of 25 millimeters in diameter at a gap of two millimeters. The top plate is attached to a dynamic motor while the bottom plate is attached to a 2000 gm-cm torque transducer of a Rheometrics® Dynamic Spectrometer or Analyzer. The test temperature is held at 200° C. While keeping the bottom plate stationary, a small amplitude oscillatory motion is imposed on the top plate sweeping the frequency range from 0.1 to 500 radian/second. At each frequency, after the transients have died out, the dynamic stress response is separable into in-phase and out-of-phase components of the shearing strain. The dynamic modulus, G', characterizes the in-phase component while the loss modulus, G", characterizes the out-of-phase component of the dynamic stress. For high molecular weight polyolefins, such as polypropylenes, it is observed that these moduli crossover at a point when measured as a function of frequency. This crossover modulus is characterized as Gc, and the crossover frequency is characterized by Wc.

The polydispersity index is defined by 10⁶ /crossover modulus, and is found to correlate with the molecular weight distribution, Mw/Mn. The crossover frequency correlates inversely with the weight average molecular weight, Mw, for polypropylenes.

Preferably, the fiber of the present invention also has a viscoelastic constant of about 1.5-2.0. The viscoelastic constant (VC) is defined according to the equation VC=η∘/(Gc/Wc)¹.21, where "η∘" is the zero shear viscosity in poise, and "Gc/Wc" is the ratio of crossover modulus to crossover frequency in poise, that is (dyne) (sec)/cm². The values of Gc and Wc are determined utilizing the dynamic shear procedure described above. However, the zero shear viscosity is determined utilizing a low shear steady shear procedure in which a cone and plate fixture are used as the platens instead of the two parallel plates in the dynamic shear procedure. More specifically, the cone has a cone angle of 0.1 radian, and both the cone and the plate are 25 mm in diameter. The test temperature is held at 200° C., as with the dynamic shear procedure. While maintaining the bottom plate stationary, a constant rotational motion is imposed on the top cone at a constant shear rate. After an elapsed time, the stress measured by the transducer maintains a constant value. The viscosity is computed from this steady stress, and the imposed shear rate. The zero shear viscosity, η∘, is defined as the viscosity of a high molecular weight polymer in which the viscosity is invariant as a function of shear rate. The zero shear viscosity is measured by performing the shear sweep from a shear rate of 0.001 sec⁻¹ to 3.0 sec⁻¹. The zero shear viscosity is obtained in the low shear rate region, and it is the viscosity that has an associated torque greater than 2 gm-cm, and does not vary with shear rate.

The filaments and fibers of the present invention have a substantially uniform structure. This structure is different from the sheath-core differential morphology that is associated with the polypropylene filaments and fibers of the above-referenced Kozulla patent applications, corresponding subject matter of which was laid open on Aug. 6, 1991 in Canadian Laid-Open Patent Application No. 2,035,575.

The substantially uniform morphological structure of the filaments and fibers according to the present invention is characterizable by transmission electron microscopy (TEM) of ruthenium tetroxide (RuO₄)-stained fiber thin sections. In this regard, as taught by Trent et al., in Macromolecules, Vol. 16, No. 4, 1983, "Ruthenium Tetroxide Staining of Polymers for Electron Microscopy", which is hereby incorporated by reference in its entirety, it is well known that the microphology of polymeric materials is dependent on their heat treatment, composition, and processing, and that, in turn, mechanical properties of these materials such as toughness, impact strength, resilience, fatigue, and fracture strength can be highly sensitive to morphology. Further, this article teaches that transmission electron microscopy is an established technique for the characterization of the structure of heterogeneous polymer systems at a high level of resolution; however, it is often necessary to enhance image contrast for polymers by use of a staining agent. Useful staining agents for polymers are taught to include osmium tetroxide and ruthenium tetroxide. For the staining of the filaments and fibers of the present invention, ruthenium tetroxide is the preferred staining agent.

In the morphological characterization of the present invention, samples of filaments or fibers are stained with aqueous RuO₄, such as a 0.5% (by weight) aqueous solution of ruthenium tetroxide obtainable from Polysciences, Inc., overnight at room temperature. (While a liquid stain is utilized in this procedure, staining of the samples with a gaseous stain is also possible.) Stained fibers are embedded in Spurr epoxy resin and cured overnight at 60° C. The embedded stained fibers are then thin sectioned on an ultramicrotome using a diamond knife at room temperature to obtain microtomed sections approximately 80 nm thick, which can be examined on conventional apparatus, such as a Zeiss EM-10 TEM, at 100 kV. Energy dispersive x-ray analysis (EDX) was utilized to confirm that the RuO₄ had penetrated completely to the center of the fiber.

Fibers that are produced according to sheath-core differential morphology of the above-referenced Kozulla applications show an enrichment of the ruthenium on the outside surface of the fiber (Ru residue), and on the outer sheath (approximately 1 μm) of the fiber cross-section. Further, the core of these Kozulla fibers show a much lower ruthenium content. In contrast, fibers that are produced according to the present invention have a more uniform distribution of ruthenium across the fiber cross-section than the fiber produced according to the sheath-core differential morphology of Kozulla, and do not illustrate a sheath-core differential morphology.

It is also preferred that the fiber of the present invention have a tenacity no greater than about 2.5 g/denier, and a fiber elongation of at least about 250%, as measured on individual fibers using a FAFEGRAPH tensile tester with a fiber gauge length of about 1.25 cm and an extension rate of about 200%/min (average of 10 fibers tested). Fiber tenacity is defined as the breaking force divided by the denier of the fiber, while fiber elongation is defined as the % elongation to break.

As discussed above, the present invention provides non-woven materials including the fibers according to the present invention thermally bonded together. By incorporating the fibers of the present invention into nonwoven materials, nonwoven materials of exceptional cross-directional strength and percent elongation can be obtained. These nonwoven materials can be used as at least one layer in various products, including hygienic products, such as sanitary napkins, incontinence products and diapers, comprising at least one liquid absorbent layer and at least one nonwoven material layer of the present invention and/or incorporating fibers of the present invention thermally bonded together. Further, as previously indicated, the articles according to the present invention can include at least one liquid impermeable layer. For example, a diaper incorporating a nonwoven fabric of the present invention would include, as a preferred embodiment, an outermost impermeable layer, an inner layer of the nonwoven material, and at least one intermediate absorbent layer. Of course, a plurality of nonwoven material layers and absorbent layers can be incorporated in the diaper (or other hygienic product) in various orientations, and a plurality of outer impermeable layers can be included for strength considerations.

In order to more clearly describe the present invention, the following non-limiting examples are provided. All parts and percentages in the examples are by weight unless indicated otherwise.

EXAMPLE 1

Fibers (2.2 dpf) are prepared using the one-step short spin process with an inside-out radial quench system. The spinnerette contains 64,030 holes, each having a diameter of 0.35 mm. Quench air velocity of about 16-30 meters/second and a spinning speed of 75 meters/minute are used. Fibers are crimped at about 8-12 crimps/cm, coated with a 0.4-0.8 fiber-weight % finish mixture of an ethoxylated fatty acid ester and an ethoxylated alcohol phosphate (available from George A. Goulston Co., Inc., Monroe, N.C., under the name LUROL PP 912), and cut into 3.8 cm long staple.

The following polymers are used. Polymer I is a homopolymer of propylene having a MFR of 20 and a PI of 4.2. Polymer II is a homopolymer of propylene having a MFR of 10 and a PI of 5.0. Polymer III is a homopolymer of propylene having a MFR of 18 and a PI of 4.6 (PV711 from Himont Canada). Polymer IV is a homopolymer of propylene having a MFR of 400±40 and a PI of 3.5±0.5 (VALTEC HH441 Himont Inc., Wilmington, Del.). Fiber samples A-H are prepared using the formulations and conditions as set forth in the following Table 1. Fiber samples B-F are examples of the present invention, and fiber samples A, G, and H are controls. Additives % are based on fiber weight.

                  TABLE 1     ______________________________________     Fiber Formulation                    Spin Temp. °C..sup.1                                 Draw Temp. °C..sup.2     ______________________________________     A   polymer I      270          49/35         0.1% IRGAFOS 168         0.1% calcium stearate         0.02% IRGANOX 1076     B   80% polymer II 270          49/32         20% polymer IV         0.06% ULTRANOX 626         0.05% calcium stearate         0.01% IRGANOX 1076     C   80% polymer II 280          51/31         20% polymer IV         0.06% ULTRANOX 626         0.05% calcium stearate         0.01% IRGANOX 1076     D   90% polymer III                        260          51/36         10% polymer IV         0.06% ULTRANOX 626         0.05% calcium stearate         0.01% IRGANOX 1076     E   85% polymer III                        260          50/36         15% polymer IV         0.06% ULTRANOX 626         0.05% calcium stearate         0.01% IRGANOX 1076     F   80% polymer II 280          51/33         20% polymer IV         0.1% IRGAFOS 168         0.05% calcium stearate         0.01% IRGANOX 1076     G   polymer II     280          49/35         0.1% EBS.sup.3         0.01% LUPERSOL 101         0.1% IRGAFOS 168         0.05% calcium stearate         0.01% IRGANOX 1076     H   polymer II     280          49/35         0.1% EBS         0.01% LUPERSOL 101         0.1% IRGAFOS 168         0.05% calcium stearate         0.01% IRGANOX 1076     ______________________________________      .sup.1 Extruder zones temperature.      .sup.2 Feedroll temperature/drawroll temperature.      .sup.3 bis(p-ethylbenzylidene) sorbitol (obtainable from Mitsui Toatsu      Chemicals, Japan).

The fiber samples are tested to determined MFR, PI, and % elongation as described hereinabove. Fibers from each sample are then made into a non-woven material (average weight 23.8 g/m²) by thermally bonding a web of the fibers at 75 m/min card bond line speed at a temperature of 150°-180° C. using a calendar roll having diamond bond points with a total bond area of about 20%. Cross-directional (CD) strength of the resulting fabric is determined by testing samples 2.5 cm wide and 12.5 cm long that have been cut in the cross direction of the fabric production. CD strength is expressed in grams of force needed to break the' fabric at the extension rate of 12.5 cm/min. Fiber and fabric test results (CD strength being for the fabric) are reported in the following Table 2.

                  TABLE 2     ______________________________________                                             Zero                                             Shear                                        CD   Visco                                        Stre-                                             sity            MFR            Draw         ngth (10.sup.4     Sample dg/min  P.I.   Ratio % Elong                                        g/in Poise)                                                   VC     ______________________________________     A      27      4.6    1.2X  378    565  1.07  1.56     B      18      5.6    1.2X  413    789  2.39  1.78     C      18      5.7    1.2X  396    683  2.36  1.76     D      25      4.8    1.35X 347    663     E      26      4.8    1.35X 409    649     F      20      5.3    1.1X  324    742     G      23      3.8    1.1X  330    470     H      23      4.1    1.3X  304    497     ______________________________________

Comparing results for samples B-F with controls A, G, and H demonstrates that the fibers of the present invention exhibit superior fabric strength and thermal bonding properties.

EXAMPLE 2

Fibers (2.2 dpf) are prepared using a one-step spinning process with a cross-blow quench system. Spinnerettes contained 30,500 0.3 mm diameter holes. Quench air velocity is about 30-35 meters per second. The spinning speed is 86 meters/minute and the drawing speed is 103 meters/minute. The fibers are crimped at about 8-12 crimps/cm and cut into 4.8 cm long staple during the same process. Polypropylene polymers III and IV of the Example I are used in these experiments. Fiber samples J and K are prepared using the formulations and conditions as set forth in the following Table 3. Fiber sample K is an example of the present invention, and fiber sample J is a control. Additives % are based on fiber weight.

                  TABLE 3     ______________________________________     Fiber Formulation                     Spin Temp. °C..sup.1                                 Draw Temp. °C..sup.2     ______________________________________     J   polymer III     235         60/60         0.06% CYANOX 1790         0.05% calcium stearate         0.1% TiO.sub.2         0.01% IRGANOX 1076     K   95% polymer III 247         60/60         5% polymer IV         0.085% ULTRANOX 626         0.07% calcium Stearate         0.14% TiO.sub.2         0.01% IRGANOX 1076     ______________________________________      .sup.1 Extruder zones temperature.      .sup.2 Feedroll temperature/drawroll temperature.

The fiber samples are tested and fabrics made and tested as in Example 1. Results are reported in the following Table 4. Again the CD strength pertains to the fabric and the other results pertain to the fiber.

                  TABLE 4     ______________________________________                                             Zero                                             Shear                                        CD   Visco                                        Stre-                                             sity            MFR            Draw         ngth (10.sup.4     Sample dg/min  P.I.   Ratio % Elong                                        g/in Poise)                                                   VC     ______________________________________     J      22      4.3    1.2X  344    600  1.35  1.58     K      21      4.7    1.2X  376    660  1.56  1.68     ______________________________________

Sample K of the present invention, which includes a broad molecular weight distribution, exhibits superior properties with respect to control J. Therefore, in one aspect of the present invention, by having a broad molecular weight distribution in the polypropylene composition that is subjected to melt spinning, superior cross-directional properties are obtained.

EXAMPLE 3

Fibers (2.2 dpf) are prepared using a two-step manufacturing process. Fiber spinning is carried out at 777 meters/minute using spinnerettes with 782 0.35 mm diameter holes. Fibers are crimped at 8-12 crimps/cm and cut into 3.8 cm long staple at a drawing speed of 120 meters/minute. Polymers II and IV of Example 1 are used. Fiber samples L and M are prepared using the formulations and conditions as set forth in the following Table 5. Fiber sample M is a example of the present invention, and fiber sample L is a control. Additives % are based on fiber weight.

                  TABLE 5     ______________________________________     Fiber Formulation                     Spin Temp. °C..sup.1                                 Draw Temp. °C..sup.2     ______________________________________     L   polymer II      285         60/60         0.085% ULTRANOX 626         0.05% calcium stearate         0.1% TiO.sub.2         0.008% LUPERSOL 101     M   80% polymer II  305         60/60         20% polymer IV         0.085% ULTRANOX 626         0.05% calcium Stearate         0.1% TiO.sub.2     ______________________________________      .sup.1 Extruder zones temperature.      .sup.2 Feedroll temperature/drawroll temperature.

The fiber samples are tested and fabrics made and tested as in Example 1. Results are reported in the following Table 6. Again, the CD strength pertains to the fabric and the other results pertain to the fiber.

                  TABLE 6     ______________________________________                              Draw    %    CD     Sample  MFR       P.I.   Ratio   Elong                                           Strength     ______________________________________     L       26        4.2    1.2X    372  410     M       20        5.4    1.2X    506  600     ______________________________________      .sup.1 Extruder zones temperature.      .sup.2 Feedroll temperature/drawroll temperature.

Sample M of the present invention exhibits superior properties with respect to control L.

Although the invention has been described with reference to particular means, materials and embodiments, it is to be understood that the invention is not limited to the particulars disclosed and extends to all equivalents within the scope of the claims. 

What is claimed:
 1. A process for spinning polypropylene filaments comprising:melt spinning a polypropylene composition having a broad molecular weight distribution through at least one spinnerette to form molten polypropylene filaments, the polypropylene composition comprises at least one polypropylene having a melt flow rate of about 0.5-30, and at least one polypropylene having a melt flow rate of about 60-1000; and quenching the molten polypropylene filaments to obtain polypropylene filaments having an average rheological polydispersity index of at least about 5.0.
 2. The process according to claim 1, wherein the spinning speed is about 30 to 200 meters per minute.
 3. The process according to claim 2, wherein the spinning speed is about 80 to 100 meters per minute.
 4. The process according to claim 2, wherein the quenching is effected to obtain a substantially immediate cooling of the molten polypropylene filaments as the molten polypropylene filaments exit the at least one spinnerette.
 5. The process according to claim 4, wherein said quenching comprises an air quench.
 6. The process according to claim 5, wherein the quench air has a velocity of about 10 to 45 meters/second, and a temperature of about 10°-40° C.
 7. The process according to claim 6, wherein the quench air has a velocity of about 25-35 meters/second.
 8. The process according to claim 7, wherein said quench air has a velocity of about 30 meters/second.
 9. The process according to claim 7, wherein said temperature is approximately is 15°-30° C.
 10. The process according to claim 9, wherein said temperature is approximately 15°-20° C.
 11. The process according to claim 7, wherein said temperature is approximately 37° C.
 12. The process according to claim 6, wherein said polypropylene filaments are continuously drawn and crimped.
 13. The process according to claim 1, wherein the spinning speed is about 500 to 5500 meters per minute.
 14. The process according to claim 13, wherein the spinning speed is about 1100 to 2000 meters per minute.
 15. The process according to claim 13, wherein the quenching is effected to obtain a substantially immediate cooling of the molten polypropylene filaments as the molten polypropylene filaments exit the at least one spinnerette.
 16. The process according to claim 15, wherein said quenching comprises an air quench.
 17. The process according to claim 16, wherein the quench air has a velocity of about 1.5-4.0 meters/second, and a temperature of about 10°-40° C.
 18. The process according to claim 17, wherein the quench air has a velocity of about 1.5-3.0 meters/second.
 19. The process according to claim 18, wherein said quench air has a velocity of about 2.0 meters/second.
 20. The process according to claim 17, wherein said temperature is approximately 15°-30° C.
 21. The process according to claim 20, wherein said temperature is approximately 15°-20° C.
 22. The process according to claim 21, wherein said temperature is approximately 37° C.
 23. The process according to claim 17, wherein said polypropylene filaments are drawn and crimped at a speed of about 50 to 250 meters per minute.
 24. The process according to claim 23, wherein said polypropylene filaments are drawn and crimped at a speed of about 150 to 200 meters per minute.
 25. The process according to claim 1, wherein said filaments have an average rheological polydispersity index of at least about 5.5.
 26. A process for spinning polypropylene filaments comprising:melt spinning a polypropylene composition having a broad molecular weight distribution through at least one spinnerette at a spinning speed of about 30 to 200 meters per minute to form molten polypropylene filaments; and quenching the molten polypropylene filaments.
 27. The process according to claim 26, wherein the spinning speed is about 80 to 100 meters per minute.
 28. The process according to claim 27, wherein the quenched filaments have an average rheological polydispersity index of at least about 4.5.
 29. The process according to claim 28, wherein said filaments have an average rheological polydispersity index of at least about 5.0.
 30. The process according to claim 29, wherein said filaments have an average rheological polydispersity index of at least about 5.5.
 31. The process according to claim 29, wherein said filaments have an average Theological polydispersity index of about 5.0-7.0.
 32. The process according to claim 26, wherein the polypropylene composition comprises at least one polypropylene having a melt flow rate of about 0.5-30, and at least one polypropylene having a melt flow rate of about 60-1000.
 33. A process for producing thermobondable filaments having an average rheological polydispersity index of at least about 4.5 which is substantially maintained throughout the process, comprising:melt spinning a polypropylene composition having a broad molecular weight distribution with an average rheological polydispersity index of at least about 4.5 through at least one spinnerette to form molten polypropylene filaments; and quenching the molten polypropylene filaments under conditions to obtain polypropylene filaments having an average rheological polydispersity index of at least about 4.5.
 34. The process according to claim 33, wherein the spinning speed is about 30 to 200 meters per minute.
 35. The process according to claim 34, wherein the spinning speed is about 80 to 100 meters per minute.
 36. The process according to claim 34, wherein the quenching is effected to obtain a substantially immediate cooling of the molten polypropylene filaments as the molten polypropylene filaments exit the at least one spinnerette.
 37. The process according to claim 36, wherein said quenching comprises an air quench.
 38. The process according to claim 37, wherein the quench air has a velocity of about 10 to 45 meters/second, and a temperature of about 10°-40° C.
 39. The process according to claim 38, wherein the quench air has a velocity of about 25-35 meters/second.
 40. The process according to claim 39, wherein said quench air has a velocity of about 30 meters/second.
 41. The process according to claim 39, wherein said temperature is approximately 15°-30° C.
 42. The process according to claim 41, wherein said temperature is approximately 15°-20° C.
 43. The process according to claim 39, wherein said temperature is approximately 37° C.
 44. The process according to claim 38, wherein said polypropylene filaments are continuously drawn and crimped.
 45. The process according to claim 33, wherein the spinning speed is about 500 to 5500 meters per minute.
 46. The process according to claim 45, wherein the spinning speed is about 1100 to 2000 meters per minute.
 47. The process according to claim 46, wherein the quenching is effected to obtain a substantially immediate cooling of the molten polypropylene filaments as the molten polypropylene filaments exit the at least one spinnerette.
 48. The process according to claim 47, wherein said quenching comprises an air quench.
 49. The process according to claim 48, wherein the quench air has a velocity of about 1.5-4.0 meters/second, and a temperature of about 10°-40° C.
 50. The process according to claim 49, wherein the quench air has a velocity of about 1.5-3.0 meters/second.
 51. The process according to claim 50, wherein said quench air has a velocity of about 2.0 meters/second.
 52. The process according to claim 49, wherein said temperature is approximately 15°-30° C.
 53. The process according to claim 52, wherein said temperature is approximately 15°-20° C.
 54. The process according to claim 53, wherein said temperature is approximately 37° C.
 55. The process according to claim 49, wherein said polypropylene filaments are drawn and crimped at a speed of about 50 to 250 meters per minute.
 56. The process according to claim 55, wherein said polypropylene filaments are drawn and crimped at a speed of about 150 to 200 meters per minute.
 57. The process according to claim 33, wherein said composition and filaments have an average rheological polydispersity index of at least about 5.0.
 58. The process according to claim 57, wherein said composition and filaments have an average rheological polydispersity index of at least about 5.5.
 59. The process according to claim 57, wherein said composition and filaments have an average rheological polydispersity index of about 5.0-7.0.
 60. A process for producing thermobondable filaments having an average rheological polydispersity index of at least about 4.5 which is substantially maintained throughout the process, comprising:melt spinning a polypropylene composition having a broad molecular weight distribution and an average rheological polydispersity index of at least about 4.5 through at least one spinnerette to form molten polypropylene filaments; and quenching the molten polypropylene filaments under conditions to obtain a substantially uniform morphology of the quenched polypropylene filaments having an average rheological polydispersity index of at least about 4.5.
 61. The process according to claim 60, wherein the spinning speed is about 30 to 200 meters per minute.
 62. The process according to claim 61, wherein the spinning speed is about 80 to 100 meters per minute.
 63. The process according to claim 61, wherein the quenching is effected to obtain a substantially immediate cooling of the molten polypropylene filaments as the molten polypropylene filaments exit the at least one spinnerette.
 64. The process according to claim 63, wherein said quenching comprises an air quench.
 65. The process according to claim 64, wherein the quench air has a velocity of about 10 to 45 meters/second, and a temperature of about 10°-40° C.
 66. The process according to claim 65, wherein the quench air has a velocity of about 25-35 meters/second.
 67. The process according to claim 66, wherein said quench air has a velocity of about 30 meters/second.
 68. The process according to claim 66, wherein said temperature is approximately 15°-30° C.
 69. The process according to claim 68, wherein said temperature is approximately 15°-20° C.
 70. The process according to claim 66, wherein said temperature is approximately 37° C.
 71. The process according to claim 65, wherein said polypropylene filaments are continuously drawn and crimped.
 72. A process for spinning polypropylene filaments comprising:melt spinning a polypropylene composition having a broad molecular weight distribution through at least one spinnerette at a spinning speed of about 30 to 200 meters per minute to form molten polypropylene filaments; and quenching the molten polypropylene filaments to obtain polypropylene filaments having an average rheological polydispersity index of at least about 4.5.
 73. The process according to claim 72, wherein the average rheological polydispersity index is at least about 5.0.
 74. The process according to claim 73, wherein the average rheological polydispersity index is at least about 5.5.
 75. The process according to claim 72, wherein said filaments have an elongation greater than about 250%.
 76. The process according to claim 72, wherein the polypropylene composition contains at least about 3.0% of at least one polypropylene having a melt flow rate of about 60-1000.
 77. The process according to claim 76, wherein the at least one polypropylene has a melt flow rate of about 200-1000.
 78. The process according to claim 76, wherein the polypropylene composition contains at least about 10.0% of at least one polypropylene having a melt flow rate of about 60-1000.
 79. The process according to claim 72, wherein the spinning speed is about 80 to 100 meters per minute.
 80. The process according to claim 72, wherein the filaments have an average melt flow rate of about 5-40.
 81. The process according to claim 80, wherein the filaments have an average melt flow rate of about 10-30.
 82. The process according to claim 81, wherein the filaments have an average melt flow rate of about 15-25.
 83. A process for spinning polypropylene filaments comprising:melt spinning a polypropylene composition having a broad molecular weight distribution, and containing at least about 3.0% of at least one polypropylene having a melt flow rate of about 60-1000, through at least one spinnerette at a spinning speed of about 30 to 200 meters per minute to form molten polypropylene filaments; and quenching the molten polypropylene filaments to obtain polypropylene filaments having an average melt flow rate of about 5-40.
 84. The process according to claim 83, wherein the average rheological polydispersity index is at least about 4.5.
 85. The process according to claim 84, wherein the average rheological polydispersity index is at least about 5.0.
 86. The process according to claim 85, wherein the average rheological polydispersity index is at least about 5.5.
 87. The process according to claim 83, wherein said filaments have an elongation greater than about 250%.
 88. The process according to claim 83, wherein the at least one polypropylene has a melt flow rate of about 200-1000.
 89. The process according to claim 83, wherein the spinning speed is about 80 to 100 meters per minute.
 90. The process according to claim 1, wherein, based on the weight of the composition, said composition comprises at least about 3.0% by weight of said at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 3.0% by weight of said at least one polypropylene having a melt flow rate of about 60-1000.
 91. The process according to claim 1, wherein, based on the weight of the composition, said composition comprises at least about 10.0% by weight of said at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 10.0% by weight of said at least one polypropylene having a melt flow rate of about 60-1000.
 92. The process according to claim 26, wherein, based on the weight of the composition, said composition comprises at least about 3.0% by weight of said at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 3.0% by weight of said at least one polypropylene having a melt flow rate of about 60-1000.
 93. The process according to claim 26, wherein, based on the weight of the composition, said composition comprises at least about 10.0% by weight of said at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 10.0% by weight of said at least one polypropylene having a melt flow rate of about 60-1000.
 94. The process according to claim 33, wherein the polypropylene composition comprises at least one polypropylene having a melt flow rate of about 0.5-30, and at least one polypropylene having a melt flow rate of about 60-1000.
 95. The process according to claim 33, wherein, based on the weight of the composition said composition comprises at least about 3.0% by weight of said at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 3.0% by weight of said at least one polypropylene having a melt flow rate of about 60-1000.
 96. The process according to claim 33, wherein, based on the weight of the composition, said composition comprises at least about 10.0% by weight of said at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 10.0% by weight of said at least one polypropylene having a melt flow rate of about 60-1000.
 97. The process according to claim 60, wherein the polypropylene composition comprises at least one polypropylene having a melt flow rate of about 0.5-30, and at least one polypropylene having a melt flow rate of about 60-1000.
 98. The process according to claim 60, wherein, based on the weight of the composition, said composition comprises at least about 3.0% by weight of said at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 3.0% by weight of said at least one polypropylene having a melt flow rate of about 60-1000.
 99. The process according to claim 60, wherein, based on the weight of the composition, said composition comprises at least about 10.0% by weight of said at least one polypropylene having a melt flow rate of about 0.5-30, and at least about 10.0% by weight of said at least one polypropylene having a melt flow rate of about 60-1000. 